Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2")
translateModel(ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001158/0.001158, allocations: 104.2 kB / 16.42 MB, free: 6.512 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001071/0.001071, allocations: 188.3 kB / 17.36 MB, free: 5.73 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.228/1.228, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo): time 0.1619/0.1619, allocations: 38 MB / 308.6 MB, free: 5.984 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.342e-05/1.343e-05, allocations: 2.281 kB / 433.6 MB, free: 14.48 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2): time 0.05215/0.05217, allocations: 65.73 MB / 499.3 MB, free: 12.52 MB / 382.1 MB
Notification: Performance of NFInst.instExpressions: time 0.2207/0.2729, allocations: 29.62 MB / 0.5166 GB, free: 3.617 MB / 398.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001838/0.2748, allocations: 65.81 kB / 0.5166 GB, free: 3.617 MB / 398.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.002446/0.2772, allocations: 0.8347 MB / 0.5174 GB, free: 3.617 MB / 398.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.01821/0.2955, allocations: 6.548 MB / 0.5238 GB, free: 3.59 MB / 398.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.01771/0.3132, allocations: 7.157 MB / 0.5308 GB, free: 3.398 MB / 398.1 MB
Notification: Performance of NFFlatten.flatten: time 0.007656/0.3209, allocations: 5.407 MB / 0.5361 GB, free: 3.289 MB / 398.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.001816/0.3227, allocations: 1.018 MB / 0.5371 GB, free: 3.23 MB / 398.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.003825/0.3265, allocations: 2.145 MB / 0.5392 GB, free: 3.223 MB / 398.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.01687/0.3434, allocations: 8.078 MB / 0.5471 GB, free: 60 kB / 398.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0008011/0.3442, allocations: 145.2 kB / 0.5472 GB, free: 60 kB / 398.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01805/0.3623, allocations: 9.063 MB / 0.5561 GB, free: 13.02 MB / 414.1 MB
Notification: Performance of combineBinaries: time 0.004613/0.367, allocations: 3.431 MB / 0.5594 GB, free: 10.2 MB / 414.1 MB
Notification: Performance of replaceArrayConstructors: time 0.002034/0.369, allocations: 2.235 MB / 0.5616 GB, free: 8.262 MB / 414.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0008418/0.3699, allocations: 274 kB / 0.5619 GB, free: 8.062 MB / 414.1 MB
Notification: Performance of FrontEnd: time 0.0002712/0.3702, allocations: 48.19 kB / 0.5619 GB, free: 8.023 MB / 414.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 322 (232)
 * Number of variables: 362 (275)
Notification: Performance of Bindings: time 0.01039/0.3806, allocations: 9.672 MB / 0.5714 GB, free: 372 kB / 414.1 MB
Notification: Performance of FunctionAlias: time 0.001581/0.3822, allocations: 1.324 MB / 0.5726 GB, free: 15.05 MB / 430.1 MB
Notification: Performance of Early Inline: time 0.006028/0.3882, allocations: 5.02 MB / 0.5776 GB, free: 10.12 MB / 430.1 MB
Notification: Performance of simplify1: time 0.0006267/0.3888, allocations: 332.9 kB / 0.5779 GB, free: 9.816 MB / 430.1 MB
Notification: Performance of Alias: time 0.004299/0.3932, allocations: 3.644 MB / 0.5814 GB, free: 5.996 MB / 430.1 MB
Notification: Performance of simplify2: time 0.0005324/0.3937, allocations: 317 kB / 0.5817 GB, free: 5.711 MB / 430.1 MB
Notification: Performance of Events: time 0.001342/0.3951, allocations: 1.193 MB / 0.5829 GB, free: 4.512 MB / 430.1 MB
Notification: Performance of Detect States: time 0.00134/0.3964, allocations: 1.243 MB / 0.5841 GB, free: 3.289 MB / 430.1 MB
Notification: Performance of Partitioning: time 0.00223/0.3987, allocations: 1.957 MB / 0.586 GB, free: 1.098 MB / 430.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (257/344)
****************************
(1)       [ALGB] (1) Real[1] source.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(2)       [DER-] (1) Real[1] $DER.pipe3.ms
(3)       [ALGB] (1) final Real[1] pipe1.fluidVolumes = {pipe1.crossAreas[1] * 10.0} .* pipe1.nParallel
(4)       [ALGB] (1) final Real[1] pipe3.fluidVolumes = {pipe3.crossAreas[1] * 10.0} .* pipe3.nParallel
(5)       [DISC] (1) Boolean $SEV_29
(6)       [DISC] (1) Boolean $SEV_28
(7)       [DISC] (1) Boolean $SEV_27
(8)       [ALGB] (1) Real[1] pipe3.Hb_flows
(9)       [DISC] (1) Boolean $SEV_26
(10)      [ALGB] (1) Real[1] pipe1.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(11)      [DISC] (1) Integer[1] pipe3.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(12)      [DISC] (1) Boolean $SEV_23
(13)      [DISC] (1) Boolean $SEV_20
(14)      [ALGB] (2) protected Real[2] pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(15)      [DISC] (1) Integer[1] pipe3.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(16)      [ALGB] (1) Real valveIncompressible1.dp_turbulent = max(valveIncompressible1.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.dynamicViscosity(valveIncompressible1.state_a) + ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.dynamicViscosity(valveIncompressible1.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valveIncompressible1.Av * max(valveIncompressible1.relativeFlowCoefficient, 0.001) * (ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.density(valveIncompressible1.state_b) + ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.density(valveIncompressible1.state_a)))) (min = 0.0, nominal = 1e5)
(17)      [DISC] (1) Boolean $TEV_0
(18)      [ALGB] (1) Real[1] pipe1.heatTransfer.Q_flows
(19)      [ALGB] (1) Real[1] pipe3.flowModel.Res_turbulent_internal = pipe3.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(20)      [ALGB] (2) Real[2] pipe1.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.flowModel.Medium.dynamicViscosity(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(21)      [ALGB] (1) Real sink.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(22)      [ALGB] (2) Real[2] pipe3.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.flowModel.Medium.dynamicViscosity(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(23)      [ALGB] (2) Real[2] pipe3.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(24)      [ALGB] (1) Real[1] pipe3.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(25)      [DISC] (1) Boolean $SEV_16
(26)      [DISC] (1) Boolean $SEV_15
(27)      [DISC] (1) Boolean $SEV_14
(28)      [ALGB] (1) stream Real[1] sink.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(29)      [ALGB] (1) Real[1] pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel
(30)      [DISC] (1) Boolean $SEV_13
(31)      [DISC] (1) Boolean $SEV_12
(32)      [DISC] (1) Boolean $SEV_11
(33)      [ALGB] (1) final Real[1] pipe1.heatTransfer.vs = pipe1.vs
(34)      [ALGB] (1) Real[1] pipe3.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(35)      [DISC] (1) protected Integer valveOpening1.last (start = 1)
(36)      [DISC] (1) Boolean $SEV_10
(37)      [ALGB] (4) Real[2, 2] pipe3.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(38)      [ALGB] (1) Real[1] pipe3.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(39)      [ALGB] (2) protected Real[2] pipe3.vsFM
(40)      [DISC] (1) protected Integer valveIncompressible1.state_b.phase (min = 0, max = 2)
(41)      [ALGB] (1) flow Real valveIncompressible1.port_b.m_flow (min = -1e5, max = 1e60)
(42)      [ALGB] (1) Real pipe3.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(43)      [ALGB] (1) Real[1] pipe3.flowModel.Ib_flows
(44)      [ALGB] (1) Real[1] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths
(45)      [ALGB] (4) Real[2, 2] pipe3.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(46)      [DISC] (1) Boolean[1] $SEV_5[$i1]
(47)      [DISC] (4) Integer[2, 2] pipe1.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(48)      [ALGB] (4) Real[2, 2] pipe3.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(49)      [ALGB] (1) protected Real valveIncompressible1.relativeFlowCoefficient
(50)      [ALGB] (1) Real[1] pipe3.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(51)      [ALGB] (1) Real[1] pipe3.Qb_flows
(52)      [DISC] (1) protected discrete Real valveOpening1.nextEventScaled (fixed = true, start = 0.0)
(53)      [ALGB] (1) Real[1] pipe1.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(54)      [DER-] (1) Real[1] $DER.pipe1.Us
(55)      [DISC] (1) Integer[1] pipe1.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(56)      [ALGB] (2) final Real[2] pipe3.flowModel.dimensions = pipe3.dimensionsFM
(57)      [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.T = {pipe3.statesFM[1].T, pipe3.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(58)      [ALGB] (4) Real[2, 2] pipe3.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(59)      [ALGB] (1) Real[1] pipe1.Hb_flows
(60)      [ALGB] (1) stream Real pipe1.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(61)      [ALGB] (1) Real pipe1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(62)      [ALGB] (1) Real[1] pipe1.flowModel.Fs_fg
(63)      [ALGB] (1) Real[1] pipe1.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(64)      [DISC] (1) Integer source.medium.state.phase (min = 0, max = 2)
(65)      [ALGB] (1) Real[1] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(66)      [ALGB] (1) Real $FUN_9
(67)      [ALGB] (1) Real $FUN_8
(68)      [DISC] (1) final input Integer[1, 1] pipe1.heatTransfer.states.phase = {pipe1.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(69)      [DISC] (1) protected discrete Real valveOpening1.nextEvent (fixed = true, start = 0.0)
(70)      [ALGB] (1) Real $FUN_7
(71)      [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.d = {pipe3.statesFM[1].d, pipe3.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(72)      [ALGB] (1) Real $FUN_6
(73)      [ALGB] (1) Real[1] pipe1.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(74)      [ALGB] (1) Real pipe1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(75)      [ALGB] (1) Real $FUN_5
(76)      [ALGB] (2) Real[2] pipe3.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(77)      [ALGB] (1) Real $FUN_4
(78)      [DER-] (1) Real[1] $DER.pipe1.ms
(79)      [ALGB] (1) flow Real pipe1.port_a.m_flow (min = -1e60, max = 1e5)
(80)      [ALGB] (1) Real $FUN_3
(81)      [ALGB] (1) protected Real[1] pipe1.dheightsFM
(82)      [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.h = {pipe3.statesFM[1].h, pipe3.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(83)      [ALGB] (1) Real $FUN_2
(84)      [ALGB] (1) Real pipe1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(85)      [ALGB] (1) Real $FUN_1
(86)      [ALGB] (1) final Real[1] pipe1.flowModel.dheights = pipe1.dheightsFM
(87)      [ALGB] (1) stream Real pipe1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(88)      [ALGB] (1) Real[1] pipe1.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(89)      [ALGB] (1) Real sink.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(90)      [DISC] (1) protected Integer valveIncompressible1.state_a.phase (min = 0, max = 2)
(91)      [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.p = {pipe3.statesFM[1].p, pipe3.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(92)      [ALGB] (1) Real sink.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(93)      [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.p = {pipe1.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(94)      [ALGB] (1) protected Real[1] pipe1.pathLengths
(95)      [ALGB] (2) Real[2] pipe1.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(96)      [DISC] (4) Integer[2, 2] pipe3.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(97)      [ALGB] (1) Real pipe1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(98)      [ALGB] (1) stream Real[1] source.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(99)      [ALGB] (1) Real[1] pipe3.flowModel.dps_fg (start = {pipe3.flowModel.p_a_start - pipe3.flowModel.p_b_start for $i1 in 1:1})
(100)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.h = {pipe1.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(101)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.d = {pipe1.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(102)     [ALGB] (1) Real valveOpening1.y
(103)     [ALGB] (1) Real[1] pipe1.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe1.mediums[1].p)}
(104)     [ALGB] (1) Real pipe3.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(105)     [ALGB] (1) Real sink.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(106)     [ALGB] (1) protected Real[1] pipe3.pathLengths
(107)     [ALGB] (2) final Real[2] pipe3.flowModel.roughnesses = pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(108)     [ALGB] (1) protected Real valveIncompressible1.minLimiter.y
(109)     [ALGB] (1) stream Real valveIncompressible1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(110)     [ALGB] (1) Real pipe1.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(111)     [ALGB] (1) Real[1] pipe3.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(112)     [ALGB] (1) protected Real[1] pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1])
(113)     [ALGB] (1) Real pipe3.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(114)     [ALGB] (1) Real $FUN_15
(115)     [ALGB] (2) final Real[2] pipe1.flowModel.dimensions = pipe1.dimensionsFM
(116)     [ALGB] (1) Real $FUN_13
(117)     [DISC] (1) Integer $FUN_12
(118)     [ALGB] (1) Real[1] pipe1.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe1.mediums[1].T)}
(119)     [ALGB] (1) Real pipe3.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(120)     [ALGB] (2) final Real[2] pipe3.flowModel.crossAreas = pipe3.crossAreasFM
(121)     [ALGB] (1) Real[1] pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths
(122)     [ALGB] (1) Real $FUN_11
(123)     [ALGB] (1) flow Real[1] pipe1.heatTransfer.heatPorts.Q_flow
(124)     [ALGB] (1) Real[1] pipe3.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(125)     [ALGB] (1) Real $FUN_10
(126)     [DER-] (2) Real[2] $DER.valveIncompressible1.filter.x
(127)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.T = {pipe1.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(128)     [DISC] (4) final input Integer[2, 2] pipe3.flowModel.states.phase = {pipe3.statesFM[1].phase, pipe3.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(129)     [ALGB] (1) Real[1] pipe3.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.heatTransfer.Medium.temperature(pipe3.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(130)     [ALGB] (1) Real[1] pipe1.Qb_flows
(131)     [DISC] (4) final input Integer[2, 2] pipe1.flowModel.states.phase = {pipe1.statesFM[1].phase, pipe1.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(132)     [ALGB] (1) Real[1] pipe1.flowModel.Fs_p
(133)     [ALGB] (1) stream Real valveIncompressible1.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(134)     [DISC] (1) protected Real valveOpening1.b
(135)     [DISC] (1) Boolean $SEV_7
(136)     [DISC] (1) protected Real valveOpening1.a
(137)     [ALGB] (1) Real[1] pipe1.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.heatTransfer.Medium.temperature(pipe1.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(138)     [ALGB] (1) Real pipe1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(139)     [DISC] (1) Boolean $SEV_4
(140)     [ALGB] (1) Real[1] pipe3.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe3.mediums[1].p)}
(141)     [ALGB] (4) Real[2, 2] pipe1.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(142)     [ALGB] (1) Real pipe3.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(143)     [ALGB] (1) Real pipe1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(144)     [ALGB] (4) Real[2, 2] pipe1.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(145)     [ALGB] (1) Real valveIncompressible1.port_a_T = Modelica.Fluid.Utilities.regStep(-valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.temperature(valveIncompressible1.state_a), ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.setState_phX(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, {}, 0, 0)), valveIncompressible1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(146)     [ALGB] (1) Real pipe1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(147)     [ALGB] (1) Real[1] pipe1.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(148)     [ALGB] (1) Real[1] pipe1.flowModel.Is
(149)     [ALGB] (1) Real[1] pipe3.flowModel.Is
(150)     [ALGB] (4) Real[2, 2] pipe1.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(151)     [ALGB] (1) protected Real valveIncompressible1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(152)     [ALGB] (2) Real[2] pipe1.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(153)     [ALGB] (1) Real[1] pipe1.flowModel.dps_fg (start = {pipe1.flowModel.p_a_start - pipe1.flowModel.p_b_start for $i1 in 1:1})
(154)     [ALGB] (1) Real[1] pipe3.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(155)     [ALGB] (1) Real[1] pipe1.mediums.p (start = {pipe1.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(156)     [ALGB] (1) final Real[1] pipe3.flowModel.pathLengths = pipe3.pathLengths
(157)     [DISC] (1) final input Integer[1, 1] pipe3.heatTransfer.states.phase = {pipe3.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(158)     [ALGB] (2) Real[2] pipe1.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(159)     [ALGB] (1) protected Real valveIncompressible1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(160)     [ALGB] (1) Real[1] pipe3.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(161)     [ALGB] (1) Real[1] pipe1.mediums.h (start = {pipe1.h_start}, StateSelect = prefer)
(162)     [ALGB] (1) Real valveIncompressible1.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(163)     [ALGB] (1) protected Real valveIncompressible1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(164)     [ALGB] (1) Real pipe1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(165)     [ALGB] (1) Real source.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(166)     [ALGB] (1) Real[1] pipe3.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(167)     [ALGB] (1) Real[1] pipe1.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(168)     [ALGB] (4) Real[2, 2] pipe1.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(169)     [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.p = {pipe3.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(170)     [ALGB] (1) Real pipe3.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(171)     [ALGB] (4) final input Real[2, 2] pipe1.flowModel.states.p = {pipe1.statesFM[1].p, pipe1.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(172)     [ALGB] (1) Real source.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(173)     [ALGB] (1) Real pipe1.port_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(174)     [ALGB] (1) final Real[1] pipe3.flowModel.dheights = pipe3.dheightsFM
(175)     [ALGB] (1) Real[1] pipe1.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(176)     [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.h = {pipe3.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(177)     [ALGB] (1) protected Real valveIncompressible1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(178)     [ALGB] (2) final Real[2] pipe1.flowModel.crossAreas = pipe1.crossAreasFM
(179)     [ALGB] (1) Real pipe3.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(180)     [ALGB] (1) Real source.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(181)     [ALGB] (4) final input Real[2, 2] pipe1.flowModel.states.h = {pipe1.statesFM[1].h, pipe1.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(182)     [ALGB] (1) Real[1] pipe3.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(183)     [ALGB] (1) Real[1] pipe3.Wb_flows
(184)     [ALGB] (1) Real[1] pipe1.mediums.T (start = {pipe1.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(185)     [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.d = {pipe3.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(186)     [ALGB] (1) Real pipe3.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(187)     [ALGB] (1) Real[1] pipe1.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(188)     [ALGB] (2) protected Real[2] pipe1.crossAreasFM
(189)     [ALGB] (1) Real source.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(190)     [ALGB] (4) final input Real[2, 2] pipe1.flowModel.states.d = {pipe1.statesFM[1].d, pipe1.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(191)     [ALGB] (1) stream Real pipe3.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(192)     [ALGB] (1) Real[1] pipe3.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(193)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_fg
(194)     [ALGB] (2) Real[2] pipe3.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.flowModel.Medium.density(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(195)     [ALGB] (2) protected Real[2] pipe3.crossAreasFM
(196)     [ALGB] (2) protected Real[2] pipe1.dimensionsFM
(197)     [ALGB] (2) protected Real[2] pipe3.dimensionsFM
(198)     [ALGB] (1) Real[1] pipe1.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(199)     [ALGB] (2) final Real[2] pipe1.flowModel.roughnesses = pipe1.roughnessesFM (min = {0.0 for $i1 in 1:2})
(200)     [ALGB] (1) Real source.medium.h (StateSelect = default)
(201)     [ALGB] (3) protected Real[3] valveIncompressible1.filter.uu
(202)     [ALGB] (1) Real[1] pipe3.mediums.p (start = {pipe3.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(203)     [ALGB] (1) Real sink.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - sink.medium.T_degC))
(204)     [ALGB] (1) Real source.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(205)     [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60)
(206)     [ALGB] (2) protected Real[2] pipe1.vsFM
(207)     [ALGB] (1) Real[1] pipe3.mediums.h (start = {pipe3.h_start}, StateSelect = prefer)
(208)     [ALGB] (1) Real source.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(209)     [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.T = {pipe3.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(210)     [ALGB] (1) Real pipe3.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(211)     [ALGB] (1) Real[1] pipe1.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(212)     [ALGB] (4) final input Real[2, 2] pipe1.flowModel.states.T = {pipe1.statesFM[1].T, pipe1.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(213)     [ALGB] (1) flow Real[1] source.ports.m_flow (min = {-1e60}, max = {1e60})
(214)     [ALGB] (1) Real[1] pipe3.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(215)     [ALGB] (1) Real[1] pipe1.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(216)     [ALGB] (1) Real[1] pipe3.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(217)     [ALGB] (2) final Real[2] pipe1.flowModel.vs = pipe1.vsFM
(218)     [ALGB] (2) final Real[2] pipe3.flowModel.vs = pipe3.vsFM
(219)     [ALGB] (1) flow Real[1] sink.ports.m_flow (min = {-1e60}, max = {1e60})
(220)     [ALGB] (1) Real[1] pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel
(221)     [ALGB] (1) Real valveIncompressible1.port_b_T = Modelica.Fluid.Utilities.regStep(valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.temperature(valveIncompressible1.state_b), ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.setState_phX(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, {}, 0, 0)), valveIncompressible1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(222)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_p
(223)     [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], ((pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]) / 2.0)[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(224)     [ALGB] (1) Real source.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - source.medium.T_degC))
(225)     [ALGB] (1) Real valveIncompressible1.V_flow = (-valveIncompressible1.port_b.m_flow) / Modelica.Fluid.Utilities.regStep(-valveIncompressible1.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.density(valveIncompressible1.state_a), ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveIncompressible1.Medium.density(valveIncompressible1.state_b), valveIncompressible1.m_flow_small)
(226)     [ALGB] (1) protected Real valveIncompressible1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(227)     [ALGB] (1) Real[1] pipe1.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(228)     [DISC] (1) Integer sink.medium.state.phase (min = 0, max = 2)
(229)     [ALGB] (1) protected Real[1] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1])
(230)     [DISC] (1) Integer source.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(231)     [ALGB] (1) Real[1] pipe1.flowModel.Ib_flows
(232)     [ALGB] (1) Real[1] pipe3.mediums.T (start = {pipe3.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(233)     [ALGB] (1) Real[1] pipe3.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe3.mediums[1].T)}
(234)     [ALGB] (1) final Real[1] pipe3.heatTransfer.vs = pipe3.vs
(235)     [ALGB] (1) protected Real valveIncompressible1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(236)     [ALGB] (1) Real[1] pipe3.heatTransfer.Q_flows
(237)     [ALGB] (1) Real sink.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(238)     [ALGB] (1) protected Real valveIncompressible1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(239)     [DISC] (1) Integer sink.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(240)     [ALGB] (1) Real valveIncompressible1.dp (start = 4e5)
(241)     [ALGB] (1) final Real[1] pipe1.flowModel.pathLengths = pipe1.pathLengths
(242)     [DISC] (1) Boolean $SEV_31
(243)     [DISC] (1) Integer pipe3.state_a.phase (min = 0, max = 2)
(244)     [DISC] (1) Boolean $SEV_30
(245)     [DISC] (1) Integer pipe1.state_a.phase (min = 0, max = 2)
(246)     [DER-] (1) Real[1] $DER.pipe3.Us
(247)     [ALGB] (1) Real sink.medium.h (StateSelect = default)
(248)     [ALGB] (1) Real[1] sink.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(249)     [ALGB] (2) protected Real[2] pipe1.roughnessesFM (min = {0.0 for $i1 in 1:2})
(250)     [ALGB] (1) flow Real[1] pipe3.heatTransfer.heatPorts.Q_flow
(251)     [ALGB] (1) protected Real valveIncompressible1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(252)     [ALGB] (1) protected Real pipe3.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], ((pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]) / 2.0)[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(253)     [ALGB] (1) Real sink.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(254)     [DISC] (1) Integer[1] pipe1.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(255)     [ALGB] (1) protected Real[1] pipe3.dheightsFM
(256)     [DISC] (1) Boolean[1] $SEV_21[$i1]
(257)     [ALGB] (1) Real[1] pipe1.Wb_flows


System Equations (235/304)
****************************
(1)       [SCAL] (1) source.ports[1].p = pipe1.port_a.p ($RES_SIM_204)
(2)       [SCAL] (1) pipe3.flowModel.Res_turbulent_internal[1] = pipe3.flowModel.Re_turbulent ($RES_BND_255)
(3)       [SCAL] (1) pipe1.vsFM[1] = ((pipe1.m_flows[1] / pipe1.state_a.d) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_120)
(4)       [ARRY] (1) pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) ($RES_BND_256)
(5)       [ARRY] (1) pipe1.m_flows[1:1] = pipe1.flowModel.m_flows[:] ($RES_SIM_121)
(6)       [SCAL] (1) sink.medium.phase = sink.medium.state.phase ($RES_SIM_82)
(7)       [ARRY] (5) pipe1.statesFM[2:2] = pipe1.mediums[:].state ($RES_SIM_122)
(8)       [ARRY] (1) pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel ($RES_BND_258)
(9)       [SCAL] (1) sink.medium.d = sink.medium.state.d ($RES_SIM_83)
(10)      [RECD] (5) pipe1.statesFM[1] = pipe1.state_a ($RES_SIM_123)
(11)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = sink.medium.state.T ($RES_SIM_84)
(12)      [SCAL] (1) sink.medium.h = sink.medium.state.h ($RES_SIM_86)
(13)      [SCAL] (1) pipe1.port_b.h_outflow = pipe1.mediums[1].h ($RES_SIM_126)
(14)      [SCAL] (1) pipe1.port_a.h_outflow = pipe1.mediums[1].h ($RES_SIM_127)
(15)      [SCAL] (1) sink.medium.u = sink.medium.h - sink.p / sink.medium.d ($RES_SIM_88)
(16)      [SCAL] (1) pipe1.port_b.m_flow = -pipe1.m_flows[2] ($RES_SIM_128)
(17)      [SCAL] (1) sink.medium.sat.psat = sink.p ($RES_SIM_89)
(18)      [SCAL] (1) pipe1.port_a.m_flow = pipe1.m_flows[1] ($RES_SIM_129)
(19)      [SCAL] (1) pipe1.state_a.phase = 0 ($RES_SIM_287)
(20)      [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[1], pipe1.flowModel.rhos[1], pipe1.flowModel.rhos[2], pipe1.flowModel.mus[1], pipe1.flowModel.mus[2], pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (pipe1.flowModel.g * pipe1.flowModel.dheights)[1], (0.5 .* (pipe1.flowModel.crossAreas[1:1] + pipe1.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe1.flowModel.roughnesses[1:1] + pipe1.flowModel.roughnesses[2:2]))[1], pipe1.flowModel.dp_small, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_281)
(21)      [SCAL] (1) pipe1.state_a.h = source.ports[1].h_outflow ($RES_SIM_288)
(22)      [SCAL] (1) $FUN_2 = sum(pipe1.flowModel.dps_fg) ($RES_$AUX_280)
(23)      [SCAL] (1) pipe1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_289)
(24)      [ARRY] (1) pipe3.heatTransfer.Ts = {pipe3.heatTransfer.states.h} ($RES_BND_260)
(25)      [ALGO] (5) ($RES_SIM_12)
(25)      [----] assert(not (valveOpening1.table[1, 1] > 0.0 or valveOpening1.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(valveOpening1.table[1, 1], 6, 0, true), AssertionLevel.error);

(25)      [----] when {time >= $PRE.valveOpening1.nextEvent, initial()} then
(25)      [----]   (valveOpening1.a, valveOpening1.b, valveOpening1.nextEventScaled, valveOpening1.last) := ($FUN_9, $FUN_10, $FUN_11, $FUN_12);
(25)      [----]   valveOpening1.nextEvent := valveOpening1.nextEventScaled;
(25)      [----] end when;

(26)      [ARRY] (1) pipe3.heatTransfer.vs = pipe3.vs ($RES_BND_261)
(27)      [SCAL] (1) valveOpening1.y = valveOpening1.a * time + valveOpening1.b ($RES_SIM_13)
(28)      [SCAL] (1) $DER.pipe3.ms[1] = pipe3.mb_flows[1] ($RES_SIM_15)
(29)      [SCAL] (1) $DER.pipe3.Us[1] = pipe3.Wb_flows[1] + pipe3.Hb_flows[1] + pipe3.Qb_flows[1] ($RES_SIM_16)
(30)      [ARRY] (10) pipe1.flowModel.states = pipe1.statesFM ($RES_BND_265)
(31)      [SCAL] (1) pipe1.H_flows[2] = -$FUN_4 ($RES_SIM_130)
(32)      [SCAL] (1) pipe3.ms[1] = pipe3.fluidVolumes[1] * pipe3.mediums[1].d ($RES_SIM_17)
(33)      [ARRY] (5) pipe1.heatTransfer.states = pipe1.mediums.state ($RES_BND_266)
(34)      [SCAL] (1) pipe1.H_flows[1] = $FUN_3 ($RES_SIM_131)
(35)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_91)
(36)      [SCAL] (1) pipe3.Us[1] = pipe3.ms[1] * pipe3.mediums[1].u ($RES_SIM_18)
(37)      [ARRY] (10) pipe3.flowModel.states = pipe3.statesFM ($RES_BND_267)
(38)      [SCAL] (1) sink.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_92)
(39)      [SCAL] (1) pipe3.port_b.p = pipe3.mediums[1].p ($RES_SIM_19)
(40)      [SCAL] (1) pipe1.mb_flows[1] = pipe1.m_flows[1] - pipe1.m_flows[2] ($RES_SIM_132)
(41)      [ARRY] (5) pipe3.heatTransfer.states = pipe3.mediums.state ($RES_BND_268)
(42)      [SCAL] (1) $FUN_3 = semiLinear(pipe1.port_a.m_flow, source.ports[1].h_outflow, pipe1.mediums[1].h) ($RES_$AUX_279)
(43)      [SCAL] (1) pipe1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_290)
(44)      [SCAL] (1) sink.medium.phase = if $SEV_10 then 1 else 2 ($RES_SIM_93)
(45)      [SCAL] (1) pipe1.Hb_flows[1] = pipe1.H_flows[1] - pipe1.H_flows[2] ($RES_SIM_133)
(46)      [SCAL] (1) $FUN_4 = semiLinear(pipe1.port_b.m_flow, pipe3.port_a.h_outflow, pipe1.mediums[1].h) ($RES_$AUX_278)
(47)      [SCAL] (1) pipe1.state_a.p = pipe1.port_a.p ($RES_SIM_291)
(48)      [ARRY] (2) pipe1.roughnessesFM[:] = {pipe1.roughnesses[1], pipe1.roughnesses[1]} ($RES_SIM_134)
(49)      [SCAL] (1) $FUN_5 = ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe3.flowModel.dps_fg[1], pipe3.flowModel.rhos[1], pipe3.flowModel.rhos[2], pipe3.flowModel.mus[1], pipe3.flowModel.mus[2], pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (pipe3.flowModel.g * pipe3.flowModel.dheights)[1], (0.5 .* (pipe3.flowModel.crossAreas[1:1] + pipe3.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe3.flowModel.roughnesses[1:1] + pipe3.flowModel.roughnesses[2:2]))[1], pipe3.flowModel.dp_small, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_277)
(50)      [ARRY] (2) pipe1.dimensionsFM[:] = {pipe1.dimensions[1], pipe1.dimensions[1]} ($RES_SIM_135)
(51)      [SCAL] (1) $FUN_6 = sum(pipe3.flowModel.dps_fg) ($RES_$AUX_276)
(52)      [SCAL] (1) pipe1.state_b.h = pipe3.port_a.h_outflow ($RES_SIM_293)
(53)      [ARRY] (2) pipe1.crossAreasFM[:] = {pipe1.crossAreas[1], pipe1.crossAreas[1]} ($RES_SIM_136)
(54)      [SCAL] (1) $FUN_7 = semiLinear(-pipe1.port_b.m_flow, pipe1.port_b.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_275)
(55)      [SCAL] (1) pipe1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe1.port_b.p, pipe3.port_a.h_outflow, 0, 0) ($RES_SIM_294)
(56)      [SCAL] (1) valveIncompressible1.dp = pipe3.port_b.p - valveIncompressible1.port_b.p ($RES_SIM_97)
(57)      [ARRY] (1) pipe1.dheightsFM[:] = {0.0} ($RES_SIM_137)
(58)      [SCAL] (1) $FUN_8 = semiLinear(valveIncompressible1.port_b.m_flow, valveIncompressible1.port_a.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_274)
(59)      [SCAL] (1) pipe1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe1.port_b.p, pipe3.port_a.h_outflow, 0, 0) ($RES_SIM_295)
(60)      [ARRY] (1) pipe1.pathLengths[:] = {10.0} ($RES_SIM_138)
(61)      [TUPL] (4) ($FUN_9, $FUN_10, $FUN_11, $FUN_12) = ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.valveOpening1.getInterpolationCoefficients(valveOpening1.table, valveOpening1.offset, valveOpening1.startTime, time, valveOpening1.last, 1e-13, valveOpening1.shiftTime) ($RES_$AUX_273)
(62)      [SCAL] (1) pipe1.state_b.p = pipe1.port_b.p ($RES_SIM_296)
(63)      [ARRY] (1) pipe1.Wb_flows = (pipe1.crossAreas * pipe1.vs * (($FUN_2 + pipe1.port_b.p) - ((system.g * {0.0}) / pipe1.mediums.d + pipe1.port_a.p))) / ({1.0} * {1.0}) .* {1.0} .* pipe1.nParallel ($RES_SIM_139)
(64)      [SCAL] (1) $FUN_13 = ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (0.5 .* (pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]))[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_272)
(65)      [SCAL] (1) valveIncompressible1.state_a.phase = 0 ($RES_SIM_297)
(66)      [SCAL] (1) pipe3.flowModel.dp_fric_nominal = sum({$FUN_13}) ($RES_$AUX_271)
(67)      [SCAL] (1) valveIncompressible1.state_a.h = valveIncompressible1.port_b.h_outflow ($RES_SIM_298)
(68)      [SCAL] (1) $FUN_15 = ModelicaTest.Fluid.TestPipesAndValves.SeriesPipes2.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (0.5 .* (pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]))[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_270)
(69)      [SCAL] (1) valveIncompressible1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) ($RES_SIM_299)
(70)      [SCAL] (1) valveIncompressible1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) ($RES_SIM_300)
(71)      [SCAL] (1) valveIncompressible1.state_a.p = pipe3.port_b.p ($RES_SIM_301)
(72)      [SCAL] (1) valveIncompressible1.state_b.phase = 0 ($RES_SIM_302)
(73)      [ARRY] (1) pipe3.vsFM[2:2] = pipe3.vs ($RES_SIM_20)
(74)      [SCAL] (1) valveIncompressible1.state_b.h = sink.ports[1].h_outflow ($RES_SIM_303)
(75)      [SCAL] (1) pipe3.vsFM[1] = ((pipe3.m_flows[1] / pipe3.state_a.d) / pipe3.crossAreas[1]) / pipe3.nParallel ($RES_SIM_21)
(76)      [SCAL] (1) valveIncompressible1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(valveIncompressible1.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_304)
(77)      [ARRY] (1) pipe3.m_flows[1:1] = pipe3.flowModel.m_flows[:] ($RES_SIM_22)
(78)      [SCAL] (1) valveIncompressible1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_305)
(79)      [ARRY] (5) pipe3.statesFM[2:2] = pipe3.mediums[:].state ($RES_SIM_23)
(80)      [SCAL] (1) valveIncompressible1.state_b.p = valveIncompressible1.port_b.p ($RES_SIM_306)
(81)      [RECD] (5) pipe3.statesFM[1] = pipe3.state_a ($RES_SIM_24)
(82)      [SCAL] (1) pipe3.state_a.phase = 0 ($RES_SIM_307)
(83)      [SCAL] (1) pipe3.state_a.h = pipe1.port_b.h_outflow ($RES_SIM_308)
(84)      [SCAL] (1) pipe3.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe1.port_b.p, pipe1.port_b.h_outflow, 0, 0) ($RES_SIM_309)
(85)      [SCAL] (1) valveIncompressible1.port_b.h_outflow = pipe3.mediums[1].h ($RES_SIM_27)
(86)      [ARRY] (1) pipe1.Qb_flows = pipe1.heatTransfer.Q_flows ($RES_SIM_140)
(87)      [SCAL] (1) pipe3.port_a.h_outflow = pipe3.mediums[1].h ($RES_SIM_28)
(88)      [ARRY] (1) pipe1.heatTransfer.Q_flows = pipe1.heatTransfer.heatPorts.Q_flow ($RES_SIM_141)
(89)      [SCAL] (1) valveIncompressible1.port_b.m_flow = -pipe3.m_flows[2] ($RES_SIM_29)
(90)      [ARRY] (1) pipe1.heatTransfer.Ts = pipe1.heatTransfer.heatPorts.T ($RES_SIM_142)
(91)      [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum({$FUN_15}) ($RES_$AUX_269)
(92)      [ARRY] (1) {0.0} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_143)
(93)      [ARRY] (1) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[1] * pipe1.flowModel.pathLengths[1]} ($RES_SIM_144)
(94)      [ARRY] (1) pipe1.flowModel.dps_fg = {(2.0 * (pipe1.flowModel.Fs_fg[1] / pipe1.flowModel.nParallel)) / (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2])} ($RES_SIM_145)
(95)      [ARRY] (1) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.5 * (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2]) * (pipe1.flowModel.states.phase - pipe1.flowModel.states.phase)} ($RES_SIM_146)
(96)      [ARRY] (1) pipe1.flowModel.Ib_flows = {0.0} ($RES_SIM_147)
(97)      [SCAL] (1) pipe1.flowModel.rhos_act[1] = noEvent(if $SEV_20 then pipe1.flowModel.rhos[1] else pipe1.flowModel.rhos[2]) ($RES_SIM_148)
(98)      [SCAL] (1) pipe1.flowModel.mus_act[1] = noEvent(if $SEV_20 then pipe1.flowModel.mus[1] else pipe1.flowModel.mus[2]) ($RES_SIM_149)
(99)      [SCAL] (1) pipe3.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe1.port_b.p, pipe1.port_b.h_outflow, 0, 0) ($RES_SIM_310)
(100)     [SCAL] (1) pipe3.state_a.p = pipe1.port_b.p ($RES_SIM_311)
(101)     [SCAL] (1) -pipe1.port_b.m_flow = pipe3.m_flows[1] ($RES_SIM_30)
(102)     [SCAL] (1) pipe3.state_b.h = valveIncompressible1.port_a.h_outflow ($RES_SIM_313)
(103)     [SCAL] (1) pipe3.H_flows[2] = -$FUN_8 ($RES_SIM_31)
(104)     [SCAL] (1) pipe3.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) ($RES_SIM_314)
(105)     [SCAL] (1) pipe3.H_flows[1] = $FUN_7 ($RES_SIM_32)
(106)     [SCAL] (1) pipe3.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) ($RES_SIM_315)
(107)     [SCAL] (1) pipe3.mb_flows[1] = pipe3.m_flows[1] - pipe3.m_flows[2] ($RES_SIM_33)
(108)     [SCAL] (1) pipe3.state_b.p = pipe3.port_b.p ($RES_SIM_316)
(109)     [SCAL] (1) pipe3.Hb_flows[1] = pipe3.H_flows[1] - pipe3.H_flows[2] ($RES_SIM_34)
(110)     [ARRY] (2) pipe3.roughnessesFM[:] = {pipe3.roughnesses[1], pipe3.roughnesses[1]} ($RES_SIM_35)
(111)     [ARRY] (2) pipe3.dimensionsFM[:] = {pipe3.dimensions[1], pipe3.dimensions[1]} ($RES_SIM_36)
(112)     [ARRY] (2) pipe3.crossAreasFM[:] = {pipe3.crossAreas[1], pipe3.crossAreas[1]} ($RES_SIM_37)
(113)     [ARRY] (1) pipe1.flowModel.m_flows = {homotopy(({$FUN_1} .* pipe1.flowModel.nParallel)[1], (pipe1.flowModel.m_flow_nominal / pipe1.flowModel.dp_nominal * (pipe1.flowModel.dps_fg - (pipe1.flowModel.g * pipe1.flowModel.dheights) .* pipe1.flowModel.rho_nominal))[1])} ($RES_SIM_150)
(114)     [ARRY] (1) pipe3.dheightsFM[:] = {0.0} ($RES_SIM_38)
(115)     [ARRY] (1) pipe3.pathLengths[:] = {10.0} ($RES_SIM_39)
(116)     [ARRY] (1) pipe1.mediums.phase = pipe1.mediums.state.phase ($RES_SIM_156)
(117)     [ARRY] (1) pipe1.mediums.d = pipe1.mediums.state.d ($RES_SIM_157)
(118)     [ARRY] (1) pipe1.mediums.T = pipe1.mediums.state.T ($RES_SIM_158)
(119)     [ARRY] (1) pipe1.mediums.p = pipe1.mediums.state.p ($RES_SIM_159)
(120)     [SCAL] (1) $TEV_0 = $PRE.valveOpening1.nextEvent ($RES_EVT_320)
(121)     [SCAL] (1) $SEV_4 = pipe3.flowModel.m_flows[1] > 0.0 ($RES_EVT_321)
(122)     [SCAL] (1) $SEV_5[1] = pipe3.mediums[1].p >= 0.0 ($RES_EVT_322)
(123)     [SCAL] (1) $SEV_7 = (pipe3.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe3.mediums.sat.psat)) or pipe3.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe3.mediums.sat.psat))) or pipe3.mediums[1].p > 2.2064e7 ($RES_EVT_324)
(124)     [SCAL] (1) $SEV_10 = (sink.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(sink.medium.sat.psat)) or sink.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(sink.medium.sat.psat))) or sink.p > 2.2064e7 ($RES_EVT_327)
(125)     [SCAL] (1) $SEV_11 = valveIncompressible1.dp >= valveIncompressible1.dp_turbulent ($RES_EVT_328)
(126)     [SCAL] (1) $SEV_12 = valveIncompressible1.state_a.d > 0.0 ($RES_EVT_329)
(127)     [ARRY] (1) pipe1.fluidVolumes = {10.0 * pipe1.crossAreas[1]} .* pipe1.nParallel ($RES_BND_211)
(128)     [ARRY] (1) pipe1.mediums.p_bar = {1e-5 * pipe1.mediums[1].p} ($RES_BND_212)
(129)     [ARRY] (1) pipe1.mediums.T_degC = {(-273.15) + pipe1.mediums[1].T} ($RES_BND_213)
(130)     [ARRY] (2) pipe1.flowModel.vs = pipe1.vsFM ($RES_BND_214)
(131)     [ARRY] (2) pipe1.flowModel.crossAreas = pipe1.crossAreasFM ($RES_BND_215)
(132)     [ARRY] (1) pipe3.Wb_flows = (pipe3.crossAreas * pipe3.vs * (($FUN_6 + pipe3.port_b.p) - ((system.g * {0.0}) / pipe3.mediums.d + pipe1.port_b.p))) / ({1.0} * {1.0}) .* {1.0} .* pipe3.nParallel ($RES_SIM_40)
(133)     [ARRY] (2) pipe1.flowModel.dimensions = pipe1.dimensionsFM ($RES_BND_216)
(134)     [ARRY] (1) pipe3.Qb_flows = pipe3.heatTransfer.Q_flows ($RES_SIM_41)
(135)     [ARRY] (2) pipe1.flowModel.roughnesses = pipe1.roughnessesFM ($RES_BND_217)
(136)     [ARRY] (1) pipe3.heatTransfer.Q_flows = pipe3.heatTransfer.heatPorts.Q_flow ($RES_SIM_42)
(137)     [ARRY] (1) pipe1.flowModel.dheights = pipe1.dheightsFM ($RES_BND_218)
(138)     [ARRY] (1) pipe3.heatTransfer.Ts = pipe3.heatTransfer.heatPorts.T ($RES_SIM_43)
(139)     [ARRY] (1) pipe1.flowModel.pathLengths = pipe1.pathLengths ($RES_BND_219)
(140)     [ARRY] (1) {0.0} = pipe3.flowModel.Ib_flows - (pipe3.flowModel.Fs_fg + pipe3.flowModel.Fs_p) ($RES_SIM_44)
(141)     [ARRY] (1) pipe3.flowModel.Is = {pipe3.flowModel.m_flows[1] * pipe3.flowModel.pathLengths[1]} ($RES_SIM_45)
(142)     [ARRY] (1) pipe3.flowModel.dps_fg = {(2.0 * (pipe3.flowModel.Fs_fg[1] / pipe3.flowModel.nParallel)) / (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2])} ($RES_SIM_46)
(143)     [ARRY] (1) pipe3.flowModel.Fs_p = pipe3.flowModel.nParallel * {0.5 * (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2]) * (pipe3.flowModel.states.phase - pipe3.flowModel.states.phase)} ($RES_SIM_47)
(144)     [ARRY] (1) pipe1.mediums.h = pipe1.mediums.state.h ($RES_SIM_160)
(145)     [ARRY] (1) pipe3.flowModel.Ib_flows = {0.0} ($RES_SIM_48)
(146)     [SCAL] (1) pipe3.flowModel.rhos_act[1] = noEvent(if $SEV_4 then pipe3.flowModel.rhos[1] else pipe3.flowModel.rhos[2]) ($RES_SIM_49)
(147)     [SCAL] (1) pipe1.mediums[1].u = pipe1.mediums[1].h - pipe1.mediums[1].p / pipe1.mediums[1].d ($RES_SIM_162)
(148)     [ARRY] (1) pipe1.mediums.sat.psat = pipe1.mediums.p ($RES_SIM_163)
(149)     [SCAL] (1) pipe1.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe1.mediums[1].p) ($RES_SIM_164)
(150)     [SCAL] (1) pipe1.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_165)
(151)     [SCAL] (1) pipe1.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_166)
(152)     [SCAL] (1) pipe1.mediums[1].phase = if $SEV_23 then 1 else 2 ($RES_SIM_167)
(153)     [SCAL] (1) source.ports[1].p = source.p ($RES_SIM_169)
(154)     [SCAL] (1) $SEV_13 = valveIncompressible1.dp <= (-valveIncompressible1.dp_turbulent) ($RES_EVT_330)
(155)     [SCAL] (1) $SEV_14 = valveIncompressible1.state_b.d > 0.0 ($RES_EVT_331)
(156)     [SCAL] (1) $SEV_15 = valveIncompressible1.state_a.d >= valveIncompressible1.state_b.d ($RES_EVT_332)
(157)     [SCAL] (1) $SEV_16 = valveOpening1.y < valveIncompressible1.minLimiter.uMin ($RES_EVT_333)
(158)     [SCAL] (1) $SEV_20 = pipe1.flowModel.m_flows[1] > 0.0 ($RES_EVT_337)
(159)     [SCAL] (1) $SEV_21[1] = pipe1.mediums[1].p >= 0.0 ($RES_EVT_338)
(160)     [FOR-] (2) ($RES_BND_220)
(160)     [----] for $i1 in 1:2 loop
(160)     [----]   [SCAL] (1) pipe1.flowModel.rhos[$i1] = pipe1.flowModel.states.d ($RES_BND_221)
(160)     [----] end for;
(161)     [FOR-] (2) ($RES_BND_222)
(161)     [----] for $i1 in 1:2 loop
(161)     [----]   [SCAL] (1) pipe1.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe1.flowModel.states.d, pipe1.flowModel.states.h, pipe1.flowModel.states.phase, pipe1.flowModel.states.p) ($RES_BND_223)
(161)     [----] end for;
(162)     [ARRY] (1) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_224)
(163)     [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[1] = pipe1.flowModel.Re_turbulent ($RES_BND_225)
(164)     [SCAL] (1) pipe3.flowModel.mus_act[1] = noEvent(if $SEV_4 then pipe3.flowModel.mus[1] else pipe3.flowModel.mus[2]) ($RES_SIM_50)
(165)     [ARRY] (1) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1]) ($RES_BND_226)
(166)     [ARRY] (1) pipe3.flowModel.m_flows = {homotopy(({$FUN_5} .* pipe3.flowModel.nParallel)[1], (pipe3.flowModel.m_flow_nominal / pipe3.flowModel.dp_nominal * (pipe3.flowModel.dps_fg - (pipe3.flowModel.g * pipe3.flowModel.dheights) .* pipe3.flowModel.rho_nominal))[1])} ($RES_SIM_51)
(167)     [ARRY] (1) pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel ($RES_BND_228)
(168)     [ARRY] (1) pipe3.mediums.phase = pipe3.mediums.state.phase ($RES_SIM_57)
(169)     [SCAL] (1) source.ports[1].h_outflow = source.medium.h ($RES_SIM_170)
(170)     [ARRY] (1) pipe3.mediums.d = pipe3.mediums.state.d ($RES_SIM_58)
(171)     [SCAL] (1) source.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(source.p, source.T, 0) ($RES_SIM_171)
(172)     [ARRY] (1) pipe3.mediums.T = pipe3.mediums.state.T ($RES_SIM_59)
(173)     [SCAL] (1) $SEV_23 = (pipe1.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe1.mediums.sat.psat)) or pipe1.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe1.mediums.sat.psat))) or pipe1.mediums[1].p > 2.2064e7 ($RES_EVT_340)
(174)     [SCAL] (1) $SEV_26 = (source.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(source.medium.sat.psat)) or source.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(source.medium.sat.psat))) or source.p > 2.2064e7 ($RES_EVT_343)
(175)     [SCAL] (1) $SEV_27 = valveIncompressible1.port_b.m_flow > valveIncompressible1.m_flow_small ($RES_EVT_344)
(176)     [SCAL] (1) $SEV_28 = valveIncompressible1.port_b.m_flow < (-valveIncompressible1.m_flow_small) ($RES_EVT_345)
(177)     [SCAL] (1) $SEV_29 = valveIncompressible1.m_flow_small > 0.0 ($RES_EVT_346)
(178)     [SCAL] (1) $SEV_30 = (-valveIncompressible1.port_b.m_flow) > valveIncompressible1.m_flow_small ($RES_EVT_347)
(179)     [SCAL] (1) $SEV_31 = (-valveIncompressible1.port_b.m_flow) < (-valveIncompressible1.m_flow_small) ($RES_EVT_348)
(180)     [ARRY] (1) pipe1.heatTransfer.Ts = {pipe1.heatTransfer.states.h} ($RES_BND_230)
(181)     [ARRY] (1) pipe1.heatTransfer.vs = pipe1.vs ($RES_BND_231)
(182)     [SCAL] (1) valveIncompressible1.V_flow = -valveIncompressible1.port_b.m_flow / smooth(1, if $SEV_30 then valveIncompressible1.state_a.d else if $SEV_31 then valveIncompressible1.state_b.d else if $SEV_29 then 0.5 * (valveIncompressible1.state_a.d + valveIncompressible1.state_b.d) - 0.25 * (valveIncompressible1.state_b.d - valveIncompressible1.state_a.d) * ((-3.0) + (valveIncompressible1.port_b.m_flow / (-valveIncompressible1.m_flow_small)) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) else 0.5 * (valveIncompressible1.state_a.d + valveIncompressible1.state_b.d)) ($RES_BND_235)
(183)     [ARRY] (1) pipe3.mediums.p = pipe3.mediums.state.p ($RES_SIM_60)
(184)     [SCAL] (1) valveIncompressible1.port_a_T = smooth(1, if $SEV_30 then valveIncompressible1.state_a.T else if $SEV_31 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) else if $SEV_29 then 0.5 * (valveIncompressible1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0) - valveIncompressible1.state_a.T) * ((-3.0) + (valveIncompressible1.port_b.m_flow / (-valveIncompressible1.m_flow_small)) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) else 0.5 * (valveIncompressible1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valveIncompressible1.port_a.h_outflow, 0, 0))) ($RES_BND_236)
(185)     [ARRY] (1) pipe3.mediums.h = pipe3.mediums.state.h ($RES_SIM_61)
(186)     [SCAL] (1) valveIncompressible1.port_a.h_outflow = sink.ports[1].h_outflow ($RES_SIM_101)
(187)     [SCAL] (1) valveIncompressible1.port_b_T = smooth(1, if $SEV_27 then valveIncompressible1.state_b.T else if $SEV_28 then Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) else if $SEV_29 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0) - valveIncompressible1.state_b.T) * ((-3.0) + (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) ^ 2.0) * (valveIncompressible1.port_b.m_flow / valveIncompressible1.m_flow_small) + 0.5 * (valveIncompressible1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0)) else 0.5 * (valveIncompressible1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valveIncompressible1.port_b.p, valveIncompressible1.port_b.h_outflow, 0, 0))) ($RES_BND_237)
(188)     [SCAL] (1) -valveIncompressible1.port_b.m_flow = homotopy(valveIncompressible1.Av * valveIncompressible1.relativeFlowCoefficient * smooth(2, if $SEV_11 then (if $SEV_12 then sqrt(valveIncompressible1.state_a.d) else 0.0) * sqrt(valveIncompressible1.dp) else if $SEV_13 then -(if $SEV_14 then sqrt(valveIncompressible1.state_b.d) else 0.0) * sqrt(abs(valveIncompressible1.dp)) else if $SEV_15 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valveIncompressible1.dp, valveIncompressible1.dp_turbulent, valveIncompressible1.state_a.d, valveIncompressible1.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valveIncompressible1.dp, valveIncompressible1.dp_turbulent, valveIncompressible1.state_b.d, valveIncompressible1.state_a.d, false, 1.0)), (valveIncompressible1.dp * valveIncompressible1.m_flow_nominal * valveIncompressible1.relativeFlowCoefficient) / valveIncompressible1.dp_nominal) ($RES_SIM_102)
(189)     [SCAL] (1) valveIncompressible1.dp_turbulent = max(valveIncompressible1.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible1.state_a.d, valveIncompressible1.state_a.T, valveIncompressible1.state_a.p, valveIncompressible1.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valveIncompressible1.state_b.d, valveIncompressible1.state_b.T, valveIncompressible1.state_b.p, valveIncompressible1.state_b.phase)) ^ 2.0) / (valveIncompressible1.Av * max(valveIncompressible1.relativeFlowCoefficient, 0.001) * (valveIncompressible1.state_b.d + valveIncompressible1.state_a.d))) ($RES_BND_238)
(190)     [SCAL] (1) pipe3.mediums[1].u = pipe3.mediums[1].h - pipe3.mediums[1].p / pipe3.mediums[1].d ($RES_SIM_63)
(191)     [ARRY] (1) pipe3.mediums.sat.psat = pipe3.mediums.p ($RES_SIM_64)
(192)     [SCAL] (1) valveIncompressible1.minLimiter.y = smooth(0, noEvent(if $SEV_16 then valveIncompressible1.minLimiter.uMin else valveOpening1.y)) ($RES_SIM_104)
(193)     [SCAL] (1) pipe3.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe3.mediums[1].p) ($RES_SIM_65)
(194)     [SCAL] (1) valveIncompressible1.relativeFlowCoefficient = valveIncompressible1.filter.u_nominal * valveIncompressible1.filter.gain * valveIncompressible1.filter.uu[3] ($RES_SIM_105)
(195)     [SCAL] (1) pipe3.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_66)
(196)     [FOR-] (2) ($RES_SIM_106)
(196)     [----] for $i1 in 1:2 loop
(196)     [----]   [SCAL] (1) valveIncompressible1.filter.uu[$i1 + 1] = valveIncompressible1.filter.x[$i1] ($RES_SIM_107)
(196)     [----] end for;
(197)     [SCAL] (1) pipe3.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_67)
(198)     [SCAL] (1) pipe3.mediums[1].phase = if $SEV_7 then 1 else 2 ($RES_SIM_68)
(199)     [SCAL] (1) source.medium.phase = source.medium.state.phase ($RES_SIM_181)
(200)     [FOR-] (2) ($RES_SIM_108)
(200)     [----] for $i1 in 1:2 loop
(200)     [----]   [SCAL] (1) $DER.valveIncompressible1.filter.x[$i1] = valveIncompressible1.filter.r[$i1] * (valveIncompressible1.filter.x[$i1] - valveIncompressible1.filter.uu[$i1]) ($RES_SIM_109)
(200)     [----] end for;
(201)     [SCAL] (1) source.medium.d = source.medium.state.d ($RES_SIM_182)
(202)     [SCAL] (1) -((-273.15) - source.medium.T_degC) = source.medium.state.T ($RES_SIM_183)
(203)     [SCAL] (1) source.medium.h = source.medium.state.h ($RES_SIM_185)
(204)     [SCAL] (1) source.medium.u = source.medium.h - source.p / source.medium.d ($RES_SIM_187)
(205)     [SCAL] (1) source.medium.sat.psat = source.p ($RES_SIM_188)
(206)     [ARRY] (1) pipe3.fluidVolumes = {10.0 * pipe3.crossAreas[1]} .* pipe3.nParallel ($RES_BND_241)
(207)     [ARRY] (1) pipe3.mediums.p_bar = {1e-5 * pipe3.mediums[1].p} ($RES_BND_242)
(208)     [ARRY] (1) pipe3.mediums.T_degC = {(-273.15) + pipe3.mediums[1].T} ($RES_BND_243)
(209)     [ARRY] (2) pipe3.flowModel.vs = pipe3.vsFM ($RES_BND_244)
(210)     [ARRY] (2) pipe3.flowModel.crossAreas = pipe3.crossAreasFM ($RES_BND_245)
(211)     [SCAL] (1) sink.ports[1].p = sink.p ($RES_SIM_70)
(212)     [SCAL] (1) valveIncompressible1.filter.uu[1] = valveIncompressible1.minLimiter.y / valveIncompressible1.filter.u_nominal ($RES_SIM_110)
(213)     [ARRY] (2) pipe3.flowModel.dimensions = pipe3.dimensionsFM ($RES_BND_246)
(214)     [SCAL] (1) sink.ports[1].h_outflow = sink.medium.h ($RES_SIM_71)
(215)     [ARRY] (2) pipe3.flowModel.roughnesses = pipe3.roughnessesFM ($RES_BND_247)
(216)     [SCAL] (1) sink.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(sink.p, sink.T, 0) ($RES_SIM_72)
(217)     [ARRY] (1) pipe3.flowModel.dheights = pipe3.dheightsFM ($RES_BND_248)
(218)     [ARRY] (1) pipe3.flowModel.pathLengths = pipe3.pathLengths ($RES_BND_249)
(219)     [SCAL] (1) $DER.pipe1.ms[1] = pipe1.mb_flows[1] ($RES_SIM_114)
(220)     [SCAL] (1) $DER.pipe1.Us[1] = pipe1.Wb_flows[1] + pipe1.Hb_flows[1] + pipe1.Qb_flows[1] ($RES_SIM_115)
(221)     [SCAL] (1) pipe1.ms[1] = pipe1.fluidVolumes[1] * pipe1.mediums[1].d ($RES_SIM_116)
(222)     [SCAL] (1) -((-273.15) - source.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_190)
(223)     [SCAL] (1) pipe1.Us[1] = pipe1.ms[1] * pipe1.mediums[1].u ($RES_SIM_117)
(224)     [SCAL] (1) source.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_191)
(225)     [SCAL] (1) pipe1.port_b.p = pipe1.mediums[1].p ($RES_SIM_118)
(226)     [SCAL] (1) source.medium.phase = if $SEV_26 then 1 else 2 ($RES_SIM_192)
(227)     [ARRY] (1) pipe1.vsFM[2:2] = pipe1.vs ($RES_SIM_119)
(228)     [SCAL] (1) pipe3.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_194)
(229)     [SCAL] (1) valveIncompressible1.port_b.m_flow + sink.ports[1].m_flow = 0.0 ($RES_SIM_196)
(230)     [SCAL] (1) pipe1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_197)
(231)     [FOR-] (2) ($RES_BND_250)
(231)     [----] for $i1 in 1:2 loop
(231)     [----]   [SCAL] (1) pipe3.flowModel.rhos[$i1] = pipe3.flowModel.states.d ($RES_BND_251)
(231)     [----] end for;
(232)     [FOR-] (2) ($RES_BND_252)
(232)     [----] for $i1 in 1:2 loop
(232)     [----]   [SCAL] (1) pipe3.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe3.flowModel.states.d, pipe3.flowModel.states.h, pipe3.flowModel.states.phase, pipe3.flowModel.states.p) ($RES_BND_253)
(232)     [----] end for;
(233)     [SCAL] (1) valveIncompressible1.port_b.p = sink.ports[1].p ($RES_SIM_202)
(234)     [SCAL] (1) pipe1.port_a.m_flow + source.ports[1].m_flow = 0.0 ($RES_SIM_203)
(235)     [ARRY] (1) pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths ($RES_BND_254)